8.1. Drag acting on a solid sphere in Stokes flow (LL)¶
Summary
Subject: Stokes drag
Main conclusion: Drag \(F_{D} = 6 \pi \mu u a\) in Stokes flow (\(Re \ll 1\)).
Key idea NS eq is linearlized by dropping the inertial term, thereby allowing the problem falls into ODE of \(f(r)\).
Reference: Derivation presented here is given by Landau and Lifshitz [LL87] (Chap. 2), but the author broke down the math path for students. See the textbook for more elegant logical strucutre.
The Navier-Stokes equation for incompressible fluids is given by
since \(\nabla \times \nabla p = 0\) by the vector identity \(\nabla \times \nabla \text{(any scalar)}\) (See Appendix Some useful identities in which some vector identities frequently used in handling equations are given). Then, the order of the differential operators can be exchanged as
Suppose that a solid sphere of radius \(a\) is fixed in a uniform flow and the far field velocity is given by \(\mathbf{u}\), which is constant (Fig. 8.1). The velocity field about the sphere can therefore be written as a superposition of \(\mathbf{u}\) and perturbation \(\mathbf{v}'\):
where \(\mathbf{A}\) is a vector potential and \(\nabla \times \mathbf{A} \rightarrow 0\) as \(r \rightarrow \infty\). Here \(r\) is the radial coordinate and the origin of the coordinate system is located at the center of the sphere. The vector potential is an axial vector and depends on the radial vector \(\mathbf{r}\) and \(\mathbf{u}\), which are both polar vectors and it should be noted that a cross product between two polar vectors becomes an axial vector (see Appendix Polar and axial vectors). Considering the boundary conditions, \(\mathbf{v} = 0~(\nabla \times \mathbf{A} = -\mathbf{u})\) at \(r = a\) and \(\mathbf{v} \rightarrow \mathbf{u}\) at \(r \rightarrow \infty\), \(\mathbf{A}\) should be proportional to \(\mathbf{u}\). Therefore, it should have the form of \(\mathbf{A} = g(r) \mathbf{e}_{r} \times \mathbf{u}\), where \(\mathbf{e}_{r} = \mathbf{r}/r\). Setting \(g(r) = df/dr\),
(8.11)¶\[ \nabla f = \frac{df}{dr} \nabla r = \frac{df}{dr} \mathbf{e}_{r} = g(r) \mathbf{e}_{r}\]
Therefore,
(8.12)¶\[ \mathbf{A} = \nabla f \times \mathbf{u}\]
Since \(\mathbf{u}\) is constant,
(8.13)¶\[ \mathbf{A}
= \nabla f \times \mathbf{u}
\rightarrow \epsilon_{ijk} \frac{\partial f}{\partial x_{j}} u_{k}
= \epsilon_{ijk} \frac{\partial f u_{k}}{\partial x_{j}}
\rightarrow \nabla \times ( f \mathbf{u} )\]
The Laplacian and the rotation in the L.H.S. is exchangeable, i.e., \(\nabla^{2} \nabla \times \mathbf{v} = \nabla \times \nabla^{2} \mathbf{v}\). However, this is zero due to Eq. (8.6). Hence,
The sum of the second and the third terms corresponds to \(\nabla \times \mathbf{A}\) and, obviously, \(\nabla \times \mathbf{A} \rightarrow 0\) as \(r \rightarrow \infty\).
Let us check the functional form of the vector potential (Fig. 8.2).
and the uniform velocity \(\mathbf{u}\) directs toward \(-z\), where \(\theta\) is the polar coordinate and \(\varphi\) is the azimuthal coordinate. Note that this definition is different from that used in Landau and Lifshitz. On the \(y\) axis (\(\theta = \pi/2\)), \(\mathbf{e}_{r} \times \mathbf{u} = - u \mathbf{e}_{x}\) and \(|\mathbf{A}|\) increases with increasing \(y\), so that \(\nabla \times \mathbf{A}\) produces vectors with direction opposite to \(\mathbf{u}\). Especially, at \(r = a\), \(\nabla \times \mathbf{A} = - \mathbf{u}\) and \(\mathbf{v} = 0\). Around the \(z\) axis (\(\theta \sim 0\)), \(\mathbf{e}_{r} \times \mathbf{u}\) gives vectors along the \(\varphi\) coordinate line. The vector field \(\mathbf{e}_{r} \times \mathbf{u}\) along the coordinate line looks rotating in the \(+\varphi\) direction, so that, roughly speaking, \(\nabla \times \mathbf{A}\) gives vectors directing toward \(+z\) so as to retard the flow around the sphere.
The pressure field can be obtained from Eq. (8.3):
(8.46)¶\[ \nabla p
= \mu \nabla^{2} ( \nabla \times \nabla \times ( f \mathbf{u} ) + \mathbf{u} )
= \mu \nabla^{2} \nabla \times \nabla \times ( f \mathbf{u} )\]
where \(\nabla^{2} \mathbf{u} = 0\) was used. Using the identity \(\nabla \times \nabla \times (\text{any vector}) = \nabla (\nabla \cdot (\text{any vector})) - \nabla^{2} (\text{any vector})\) and making some interchange in the order of the differential operators yields
(8.47)¶\[ \nabla p
= \nabla \mu \nabla^{2} \nabla \cdot f \mathbf{u} - \mu \mathbf{u} \nabla^{2} \nabla^{2} f\]
Using \(\nabla r^{n} = n r^{n-1} \mathbf{e}_{r}\) and \(\alpha = 3a/4\), we have
(8.52)¶\[ p = p_{0} - \frac{3 \mu a ( \mathbf{u} \cdot \mathbf{e}_{r} )}{2 r^{2}}\]
The drag force acting of the sphere is calculated in the following. The velocity components are (refer Fig. 8.3 for the calculation of the dot products between the velocity and the base vectors.)
where \(\tau_{\varphi r} = 0\) because of the symmetry of the flow, and \(\mathbf{e}_{z} \cdot \mathbf{e}_{r} = \cos \theta\) and \(\mathbf{e}_{z} \cdot \mathbf{e}_{\theta} = -\sin \theta\) were used. Putting this result into the integration yields